Control of a fluid catalytic cracking unit based on proportional-integral reduced order observers

Abstract The fluid catalytic cracking (FCC) unit is one of the most complex interactive processes in the refining industry, and is difficult to operate and control. This work deals with the regulative control law design for stabilization of the reactor and regenerator temperatures, considering that the kinetics terms are poorly known. The proposed control law makes use of on-line estimates of the input/output modeling errors, obtained from a proportional-integral reduced order observer. The structure of the proposed controller is similar to a proportional-double integral compensator (PI 2 ) such that a new parameterization of the controllers gains is given in terms of the closed-loop and estimation time constants. The performance of the control scheme proposed here is analyzed via numerical simulations.

[1]  H. Khalil,et al.  Output feedback stabilization of fully linearizable systems , 1992 .

[2]  Jose Alvarez-Ramirez,et al.  Robust regulation of temperature in reactor-regenerator fluid catalytic cracking units , 1996 .

[3]  V. Weekman,et al.  Kinetics of catalytic cracking selectivity in fixed, moving, and fluid bed reactors , 1970 .

[4]  Sigurd Skogestad,et al.  Procedure for regulatory control structure selection with application to the FCC process , 1993 .

[5]  William L. Luyben,et al.  Design of low-frequency compensators for improvement of plantwide regulatory performance , 1997 .

[6]  A. Arbel,et al.  Dynamics and Control of Fluidized Catalytic Crackers. 4. The Impact of Design on Partial Control , 1997 .

[7]  M. Corless,et al.  A new class of stabilizing controllers for uncertain dynamical systems , 1982, 1982 21st IEEE Conference on Decision and Control.

[8]  Hans Schuler,et al.  Calorimetric-state estimators for chemical reactor diagnosis and control: review of methods and applications , 1992 .

[9]  A. Isidori Nonlinear Control Systems , 1985 .

[10]  Said S.E.H. Elnashaie,et al.  Nonlinear Model Predictive Control of Industrial Type IV Fluid Catalytic Cracking (FCC) Units for Maximum Gasoline Yield , 1997 .

[11]  J. Gauthier,et al.  High gain estimation for nonlinear systems , 1992 .

[12]  Ronald C. Sorensen,et al.  Modifications to model IV fluid catalytic cracking units to improve dynamic performance , 1995 .

[13]  Christos Georgakis,et al.  Online Estimation of Reaction Rates in Semicontinuous Reactors , 1995 .

[14]  Leonard A. Gould,et al.  Optimal control of fluid catalytic cracking processes , 1970 .

[15]  Dag Ljungquist,et al.  State-space predictive control , 1992 .

[16]  Petteri Heinonen,et al.  FCC unit reactor-regenerator control , 1993 .

[17]  Jose Alvarez-Ramirez,et al.  Temperature regulation of a class of continuous chemical reactor based on a nonlinear Luenberger‐like observer , 1997 .

[18]  A. Errazu,et al.  A fluidized bed catalytic cracking regenerator model , 1979 .

[19]  C. Kravaris,et al.  Robust nonlinear state feedback under structured uncertainty , 1988 .

[20]  F. R. Groves,et al.  Mathematical Model of the Fluidized Bed Catalytic Cracking Plant , 1985 .